EP4303047A1 - Transport refrigeration unit with heat island mitigation - Google Patents
Transport refrigeration unit with heat island mitigation Download PDFInfo
- Publication number
- EP4303047A1 EP4303047A1 EP23183165.2A EP23183165A EP4303047A1 EP 4303047 A1 EP4303047 A1 EP 4303047A1 EP 23183165 A EP23183165 A EP 23183165A EP 4303047 A1 EP4303047 A1 EP 4303047A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- water
- refrigeration system
- refrigeration
- refrigerant
- transportation
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000005057 refrigeration Methods 0.000 title claims abstract description 166
- 230000000116 mitigating effect Effects 0.000 title 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 110
- 239000003507 refrigerant Substances 0.000 claims abstract description 103
- 230000003416 augmentation Effects 0.000 claims abstract description 46
- 238000010521 absorption reaction Methods 0.000 claims abstract description 19
- 238000004891 communication Methods 0.000 claims abstract description 13
- 230000006835 compression Effects 0.000 claims abstract description 12
- 238000007906 compression Methods 0.000 claims abstract description 12
- 239000012530 fluid Substances 0.000 claims abstract description 12
- 238000000034 method Methods 0.000 claims abstract description 12
- 239000000446 fuel Substances 0.000 claims description 44
- 238000001816 cooling Methods 0.000 claims description 30
- 239000000463 material Substances 0.000 claims description 12
- 230000001351 cycling effect Effects 0.000 claims description 9
- 238000001704 evaporation Methods 0.000 claims description 9
- 230000008020 evaporation Effects 0.000 claims description 9
- 230000000845 anti-microbial effect Effects 0.000 claims description 5
- 239000004599 antimicrobial Substances 0.000 claims description 5
- 239000003570 air Substances 0.000 description 43
- 230000005611 electricity Effects 0.000 description 14
- 239000007789 gas Substances 0.000 description 13
- 238000004146 energy storage Methods 0.000 description 12
- 239000002828 fuel tank Substances 0.000 description 10
- 239000003990 capacitor Substances 0.000 description 8
- 238000012546 transfer Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- 239000001257 hydrogen Substances 0.000 description 7
- 229910052739 hydrogen Inorganic materials 0.000 description 7
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- 230000000153 supplemental effect Effects 0.000 description 6
- 239000007921 spray Substances 0.000 description 5
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- 230000001143 conditioned effect Effects 0.000 description 4
- 229910001431 copper ion Inorganic materials 0.000 description 4
- 229910052709 silver Inorganic materials 0.000 description 4
- 239000004332 silver Substances 0.000 description 4
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000003792 electrolyte Substances 0.000 description 3
- 230000001976 improved effect Effects 0.000 description 3
- 230000000670 limiting effect Effects 0.000 description 3
- -1 silver ions Chemical class 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 239000003502 gasoline Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000007800 oxidant agent Substances 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 239000012782 phase change material Substances 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 235000010627 Phaseolus vulgaris Nutrition 0.000 description 1
- 244000046052 Phaseolus vulgaris Species 0.000 description 1
- 239000012080 ambient air Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000003190 augmentative effect Effects 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000003985 ceramic capacitor Substances 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 235000013365 dairy product Nutrition 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000002242 deionisation method Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 235000013601 eggs Nutrition 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000006870 function Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 239000003949 liquefied natural gas Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910001416 lithium ion Inorganic materials 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000010445 mica Substances 0.000 description 1
- 229910052618 mica group Inorganic materials 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 235000014571 nuts Nutrition 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- 230000002829 reductive effect Effects 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 238000002525 ultrasonication Methods 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60H—ARRANGEMENTS OF HEATING, COOLING, VENTILATING OR OTHER AIR-TREATING DEVICES SPECIALLY ADAPTED FOR PASSENGER OR GOODS SPACES OF VEHICLES
- B60H1/00—Heating, cooling or ventilating [HVAC] devices
- B60H1/32—Cooling devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60P—VEHICLES ADAPTED FOR LOAD TRANSPORTATION OR TO TRANSPORT, TO CARRY, OR TO COMPRISE SPECIAL LOADS OR OBJECTS
- B60P3/00—Vehicles adapted to transport, to carry or to comprise special loads or objects
- B60P3/20—Refrigerated goods vehicles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60H—ARRANGEMENTS OF HEATING, COOLING, VENTILATING OR OTHER AIR-TREATING DEVICES SPECIALLY ADAPTED FOR PASSENGER OR GOODS SPACES OF VEHICLES
- B60H1/00—Heating, cooling or ventilating [HVAC] devices
- B60H1/32—Cooling devices
- B60H1/3233—Cooling devices characterised by condensed liquid drainage means
- B60H1/32331—Cooling devices characterised by condensed liquid drainage means comprising means for the use of condensed liquid, e.g. for humidification or for improving condenser performance
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60H—ARRANGEMENTS OF HEATING, COOLING, VENTILATING OR OTHER AIR-TREATING DEVICES SPECIALLY ADAPTED FOR PASSENGER OR GOODS SPACES OF VEHICLES
- B60H1/00—Heating, cooling or ventilating [HVAC] devices
- B60H1/00007—Combined heating, ventilating, or cooling devices
- B60H1/00014—Combined heating, ventilating, or cooling devices for load cargos on load transporting vehicles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60H—ARRANGEMENTS OF HEATING, COOLING, VENTILATING OR OTHER AIR-TREATING DEVICES SPECIALLY ADAPTED FOR PASSENGER OR GOODS SPACES OF VEHICLES
- B60H1/00—Heating, cooling or ventilating [HVAC] devices
- B60H1/00642—Control systems or circuits; Control members or indication devices for heating, cooling or ventilating devices
- B60H1/00735—Control systems or circuits characterised by their input, i.e. by the detection, measurement or calculation of particular conditions, e.g. signal treatment, dynamic models
- B60H1/00785—Control systems or circuits characterised by their input, i.e. by the detection, measurement or calculation of particular conditions, e.g. signal treatment, dynamic models by the detection of humidity or frost
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60H—ARRANGEMENTS OF HEATING, COOLING, VENTILATING OR OTHER AIR-TREATING DEVICES SPECIALLY ADAPTED FOR PASSENGER OR GOODS SPACES OF VEHICLES
- B60H1/00—Heating, cooling or ventilating [HVAC] devices
- B60H1/32—Cooling devices
- B60H1/3204—Cooling devices using compression
- B60H1/3232—Cooling devices using compression particularly adapted for load transporting vehicles
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60H—ARRANGEMENTS OF HEATING, COOLING, VENTILATING OR OTHER AIR-TREATING DEVICES SPECIALLY ADAPTED FOR PASSENGER OR GOODS SPACES OF VEHICLES
- B60H1/00—Heating, cooling or ventilating [HVAC] devices
- B60H1/00357—Air-conditioning arrangements specially adapted for particular vehicles
- B60H1/00385—Air-conditioning arrangements specially adapted for particular vehicles for vehicles having an electrical drive, e.g. hybrid or fuel cell
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60H—ARRANGEMENTS OF HEATING, COOLING, VENTILATING OR OTHER AIR-TREATING DEVICES SPECIALLY ADAPTED FOR PASSENGER OR GOODS SPACES OF VEHICLES
- B60H1/00—Heating, cooling or ventilating [HVAC] devices
- B60H1/32—Cooling devices
- B60H2001/3286—Constructional features
- B60H2001/3289—Additional cooling source
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2250/00—Fuel cells for particular applications; Specific features of fuel cell system
- H01M2250/20—Fuel cells in motive systems, e.g. vehicle, ship, plane
Definitions
- the embodiments herein generally relate to transport refrigeration.
- Refrigerated vehicles, containers and trailers are commonly used to transport perishable goods.
- a transport refrigeration unit is commonly mounted to the vehicle, container, or to the trailer in operative association with a cargo space defined within the vehicle, container or trailer for maintaining one or more controlled temperature environments within the cargo space.
- transport refrigeration units used in connection with refrigerated vehicles and refrigerated trailers include a refrigerant compressor, a condenser with one or more associated condenser fans, an expansion device, and one or more evaporators with one or more associated evaporator fans, which are connected via appropriate refrigerant lines in a closed refrigerant flow circuit.
- Air or an air/ gas mixture is drawn from the interior volume of the cargo space by means of the evaporator fan(s) associated with the evaporator, passed through the airside of the evaporator in heat exchange relationship with refrigerant whereby the refrigerant absorbs heat from the air, thereby cooling the air.
- the cooled air is then supplied back to the cargo space.
- each compartment may have an evaporator and an associated evaporator fan.
- Heat from a truck connected to the refrigerated trailer or container can make the area between the truck and refrigerated trailer or container approximately 10°C or more higher than the ambient environment. Given the fact that the condenser is typically located in this area, the increased temperature of this area (typically referred to as a heat island) makes the transfer of heat from the refrigerant in the condenser to the surrounding air more difficult. Improved methods of transferring heat from the refrigerant in the condenser are desired.
- the present invention provides a transportation refrigeration system including:a transportation refrigeration unit configured to maintain a temperature in a refrigerated cargo space and comprising a refrigerant expansion device, a refrigerant heat absorption heat exchanger, a refrigerant compression device, and a refrigerant heat rejection heat exchanger; and a refrigeration augmentation unit comprising a water tank having an outlet, and a water droplet generator in fluid communication with a water tank outlet and configured to disperse water droplets into an air stream flowing to the refrigerant heat rejection heat exchanger.
- further embodiments may include a fuel cell having an exhaust gas outlet in fluid communication with the water tank.
- further embodiments may include a refrigeration augmentation unit which is removable.
- further embodiments may include a deionizer disposed between the water tank and the water droplet generator.
- further embodiments may include the refrigeration augmentation unit including an antimicrobial material.
- further embodiments may include the water tank having an inlet connected to an exhaust gas outlet of a fuel cell that is part of a propulsion motor.
- further embodiments may include the transportation refrigeration unit located in a heat island.
- the present invention provides a transportation refrigeration system including a transportation refrigeration unit configured to maintain a temperature in a refrigerated cargo space and comprising a refrigerant expansion device, refrigerant heat absorption heat exchanger, a refrigerant compression device, and a refrigerant heat rejection heat exchanger; a refrigeration augmentation unit comprising a water tank having an inlet, an outlet, a water droplet generator in fluid communication with the water tank outlet and configured to disperse water droplets into an air stream flowing to the refrigerant heat rejection heat exchanger; and a controller which controls the operation of the refrigeration augmentation unit based on ambient conditions and transportation refrigeration system conditions to disperse water droplets in a quantity and size that will result in evaporation of greater than or equal to 75% of the water droplets evaporate before contact with the refrigerant heat rejection heat exchanger.
- further embodiments may include a fuel cell having an exhaust gas outlet in fluid communication with the inlet of the water tank.
- further embodiments may include a deionizer disposed between the water tank and the spray nozzle.
- further embodiments may include the refrigeration augmentation unit further including an antimicrobial material.
- further embodiments may include the water tank having an inlet connected to an exhaust gas of a fuel cell located as part of a propulsion motor.
- controller configured control operation such that greater than or equal to 90% of the water droplets evaporate before contact with the refrigerant heat rejection heat exchanger.
- the water droplet generator includes an ultrasonic droplet generator.
- the present invention provides a method of cooling a refrigerated cargo space including: cycling a transportation refrigeration system on and off for a specified number of times wherein the transportation refrigeration system has a fuel cell, a controller, and a refrigeration augmentation unit and cycling is without using the refrigeration augmentation unit; and collecting water from the fuel cell during the transportation refrigeration system cycling without using the refrigeration augmentation unit; and cycling the transportation refrigeration system using the refrigeration augmentation unit, wherein water used by the refrigeration augmentation unit is the collected water.
- water may also be collected from a propulsion motor fuel cell.
- water may also be collected from a refrigerant heat absorption heat exchanger.
- the controller may control the operation of the refrigeration augmentation unit based on ambient conditions and transportation refrigeration system conditions to disperse water droplets in a quantity and size that will result in evaporation of greater than or equal to 75% of the water droplets evaporate before contact with the refrigerant heat rejection heat exchanger.
- the transportation refrigeration system may be located in a heat island.
- the compressor, and typically other components of the transport refrigeration unit is powered during transit by a prime mover, either through a direct mechanical coupling or a belt drive.
- the transport refrigeration unit may be electrically powered (e.g., using an alternating current (AC) synchronous generator that generates AC power).
- the generated AC power is typically used to power an electric motor for driving the refrigerant compressor, and other components of the transport refrigeration unit.
- the AC generator may be replaced with a battery pack to provide power to the loads.
- a fuel cell may provide power to the loads.
- the condenser of the transport refrigeration unit is typically located on the outside wall of the trailer in the area between the trailer and the truck. This area has temperatures that may be greater than or equal to 10°C higher than the ambient outdoor temperature, creating a heat island and making heat transfer from the refrigerant to the ambient outdoor less energetically favorable, decreasing the efficiency of the refrigeration unit as a whole.
- Improved heat transfer at the condenser can be achieved by incorporating evaporative cooling at the refrigerant heat rejection heat exchanger (condenser).
- Condenser refrigerant heat rejection heat exchanger
- Water droplets are sprayed onto the refrigerant heat rejection heat exchanger or into the air directly adjacent to the refrigerant heat rejection heat exchanger. Most or all of the water evaporates, and the phase change decreases the air temperature.
- the lower temperature air can accept more heat than the higher temperature air which increases the amount of heat that can be removed from the refrigerant in the refrigerant heat rejection heat exchanger.
- the resulting increase in the temperature difference between the condenser and the air flowing across the condenser results in an increase in the heat transfer rate. With increased heat transfer rate, the energy efficiency of the system overall is improved.
- water may be provided from an externally filled tank, collected from the refrigerant heat absorption heat exchanger(s) (evaporator(s)) or both.
- water may be provided by the exhaust gas of the fuel cell system optionally in combination with water collected from the refrigerant heat absorption heat exchanger, for example when water is collected during a defrost operation(s).
- a truck and trailer combination may include a truck using a fuel cell system as a power source and water from the exhaust gas of the truck fuel cell system may provide water to the refrigerant heat rejection heat exchanger water spray.
- FIG. 1 shows a schematic illustration of a transport refrigeration system 200.
- FIG. 2 shows an enlarged schematic illustration of the transport refrigeration system 200 of FIG. 1 .
- the transport refrigeration system 200 is being illustrated as a trailer system 100, as seen in FIG. 1 .
- the trailer system 100 includes a vehicle 102 coupled to a transport container 106.
- the vehicle 102 may include an operator's compartment or cab 104 and a propulsion motor 120 which acts as the drive system of the trailer system 100.
- the propulsion motor 120 is configured to power the vehicle 102.
- the energy source that powers the propulsion motor 120 may be at least one of compressed natural gas, liquefied natural gas, gasoline, electricity, diesel, hydrogen, electricity from a fuel cell, electricity from a hydrogen fueled proton exchange membrane (PEM) fuel cell, electricity from a battery, electricity from a generator, or any combination thereof.
- PEM hydrogen fueled proton exchange membrane
- the propulsion motor 120 may be an electric motor or a hybrid motor (e.g., a combustion engine and an electric motor).
- the transport container 106 may be removably coupled to the vehicle 102.
- the transport container 106 is a refrigerated trailer and includes a top wall 108, a directly opposed bottom wall 110, opposed side walls 112, and a front wall 114, with the front wall 114 being closest to the vehicle 102.
- the transportation refrigeration unit 22 is located on the front wall 114, between the transport container 106 and the vehicle 102. This placement results in the transportation refrigeration unit being located in a heat island.
- Heat island as used herein, describes an area or space in which has a temperature at least 5-10°C higher than the ambient temperature.
- the transport container 106 further includes a door or doors 117 at a rear wall 116, opposite the front wall 114.
- door or doors 117 may be located on one or more side walls 112. It is further contemplated that door or doors 117 may be located on a combination of side wall(s) 112 and rear wall 116.
- the walls of the transport container 106 define a refrigerated cargo space 119.
- the refrigerated cargo space 119 may comprise multiple compartments which may have different desired conditions such as different temperatures. For simplicity, a single refrigerated cargo space 119 is referred to herein.
- tractor-trailer refrigerated system or non-trailer refrigeration such as, for example a rigid truck, a truck having refrigerated compartment, or a shipping container having a refrigerated compartment.
- transport refrigeration systems 200 are used to transport and distribute perishable goods and environmentally sensitive goods (herein referred to as perishable goods 118).
- the perishable goods 118 may include but are not limited to fruits, vegetables, grains, beans, nuts, eggs, dairy, seed, flowers, meat, poultry, fish, ice, blood, pharmaceuticals, or any other suitable cargo requiring temperature controlled transport.
- the transport refrigeration system 200 includes a transport refrigeration unit 22, a refrigerant compression device 32, an electric motor 26 for driving the refrigerant compression device 32, and a controller 30. While shown as a single controller, controller 30 may comprise one or more sub controllers (not shown) which are coordinated to control elements of the transport refrigeration system 200.
- the transport refrigeration unit 22 is in operative association with the refrigerated cargo space 119 and is configured to provide conditioned air to the transport container 106.
- the transport refrigeration unit 22 functions, under the control of the controller 30, to establish and regulate a desired environmental parameters, such as, for example temperature, pressure, humidity, carbon dioxide, ethylene, ozone, light exposure, vibration exposure, and other conditions in the refrigerated cargo space 119, as known to one of ordinary skill in the art.
- the transport refrigeration unit 22 is capable of providing a desired temperature, carbon dioxide, and humidity range.
- the transport refrigeration unit 22 includes a refrigerant compression device 32, a refrigerant heat rejection heat exchanger (also referred to as a condenser) 34, an expansion device 36, and a refrigerant heat absorption heat exchanger (also referred to as an evaporator) 38 connected in refrigerant flow communication in a closed loop refrigerant circuit and arranged in a conventional refrigeration cycle.
- the transport refrigeration unit 22 also includes one or more fans 40 associated with the refrigerant heat rejection heat exchanger 34 and driven by fan motor(s) 42 and one or more fans 44 associated with the refrigerant heat absorption heat exchanger 38 and driven by fan motor(s) 46.
- the transport refrigeration unit 22 may also include a heater (not shown) associated with the refrigerant heat absorption heat exchanger 38.
- the heater may be an electric resistance heater. It is to be understood that other components (not shown) may be incorporated into the refrigerant circuit as desired, including for example, but not limited to, a suction modulation valve, a receiver, a filter/dryer, a sub cooler, and an economizer circuit.
- the refrigerant heat rejection heat exchanger 34 may, for example, comprise one or more refrigerant conveying coiled tubes or one or more tube banks formed of a plurality of refrigerant conveying tubes across flow path to the heat outlet 142.
- the fan(s) 40 are operative to pass air, typically ambient air, across the tubes of the refrigerant heat rejection heat exchanger 34 to cool refrigerant vapor passing through the tubes.
- the refrigerant heat rejection heat exchanger 34 may operate either as a refrigerant condenser, such as if the transport refrigeration unit 22 is operating in a subcritical refrigerant cycle or as a refrigerant gas cooler, such as if the transport refrigeration unit 22 is operating in a transcritical cycle.
- a sub cooler when present, receives refrigerant from the refrigerant heat rejection heat exchanger.
- the refrigerant heat absorption heat exchanger 38 may, for example, also comprise one or more refrigerant conveying coiled tubes or one or more tube banks formed of a plurality of refrigerant conveying tubes extending across flow path from a return air intake 136.
- the fan(s) 44 are operative to pass air drawn from the refrigerated cargo space 119 across the tubes of the refrigerant heat absorption heat exchanger 38 to heat and evaporate refrigerant liquid passing through the tubes and cool the air.
- the air cooled in traversing the refrigerant heat absorption heat exchanger 38 is supplied back to the refrigerated cargo space 119 through a refrigeration unit outlet 140.
- air when used herein with reference to the atmosphere within the cargo box includes mixtures of air with other gases, such as for example, but not limited to, nitrogen or carbon dioxide, sometimes introduced into a refrigerated cargo box for transport of perishable produce.
- Airflow is circulated into and through the refrigerated cargo space 119 of the transport container 106 by means of the transport refrigeration unit 22.
- a return airflow 134 flows into the transport refrigeration unit 22 from the refrigerated cargo space 119 through the refrigeration unit return air intake 136, and across the refrigerant heat absorption heat exchanger 38 via the fan 44, thus conditioning the return airflow 134 to a selected or predetermined temperature.
- the conditioned return airflow 134 now referred to as supply airflow 138, is supplied into the refrigerated cargo space 119 of the transport container 106 through the refrigeration unit outlet 140.
- Heat 135 is removed from the refrigerant heat rejection heat exchanger 34 through the heat outlet 142.
- the transport refrigeration unit 22 may contain an external air inlet 144, as shown in FIG. 2 , to aid in the removal of heat 135 from the refrigerant heat rejection heat exchanger 34 by pulling in external air 137.
- the supply airflow 138 may cool the perishable goods 118 in the refrigerated cargo space 119 of the transport container 106.
- the transport refrigeration unit 22 can further be operated in reverse to warm the transport container 106 when, for example, the outside temperature is very low.
- the return air intake 136, the refrigeration unit outlet 140, the heat outlet 142, and the external air inlet 144 are configured as grilles to help prevent foreign objects from entering the transport refrigeration unit 22.
- the transport refrigeration system 200 also includes a controller 30 configured for controlling the operation of the transport refrigeration system 200 including, but not limited to, the operation of various components of the refrigerant unit 22 to provide and maintain a desired thermal environment within the refrigerated cargo space 119.
- the controller 30 may also be able to selectively operate the electric motor 26.
- the controller 30 may also be configured to provide a feedforward signal to the fuel cell 400 so that it will start up before the transport refrigeration unit 22 places a load on the fuel cell 400.
- controller 30 may comprises one or more sub controllers.
- the controller 30 may be an electronic controller including a processor and an associated memory comprising computer-executable instructions that, when executed by the processor, cause the processor to perform various operations.
- the processor may be but is not limited to a single-processor or multi-processor system of any of a wide array of possible architectures, including field programmable gate array (FPGA), central processing unit (CPU), application specific integrated circuits (ASIC), digital signal processor (DSP) or graphics processing unit (GPU) hardware arranged homogenously or heterogeneously.
- the memory may be a storage device such as, for example, a random access memory (RAM), read only memory (ROM), or other electronic, optical, magnetic or any other computer readable medium.
- the controller 30 may have multiple inputs (e.g.
- the controller may also have circuits to protect the controller from inductive loads.
- the communication interface may include an interface that allows data about the operation of the transport refrigeration system to be transmitted to a remote server (e.g., the cloud) for storage and/or analysis and which also can be used to receive instructions from a remote location e.g., a remote operator or a remote server. Exemplary instructions include initiating operation of the refrigeration augmentation unit and halting operation of the refrigeration augmentation unit.
- the transport refrigeration system 200 also includes a refrigeration augmentation unit 300.
- Refrigeration augmentation unit includes a water tank 310 and a water droplet generator(s) 360 for dispersing water droplets into the air stream flowing to the refrigerant heat rejection exchanger 34, directly on the surface of the refrigerant heat rejection exchanger 34, or a combination thereof.
- the refrigerant heat rejection exchanger includes a sub cooler (not shown) the water droplets may be dispersed in the airstream flowing to the sub cooler, directly on the surface of the sub cooler, or a combination thereof.
- Exemplary water droplet generators include spray nozzles and ultrasonic droplet generators such as ultrasonication mist generators. Exemplary maximum droplet size is less than or equal to 100 micrometers ( ⁇ m), or less than or equal to 50 ⁇ m.
- the water droplet generator(s) may disperse the water droplets in any combination of orientations. In some embodiments, a combination of orientations is desired to facilitate mixing with the air flow and facilitate evaporation.
- Water droplet evaporation reduces the temperature of the air passing over the refrigerant heat rejection exchanger. By reducing the temperature of the air passing over the refrigerant heat rejection exchanger 34 the heat transfer rate from the refrigerant passing through the refrigerant heat rejection exchanger 34 can be increased.
- the water droplets are sized so that at least 75%, or at least 85%, or at least 90 volume% (vol%) of the droplets evaporate.
- the size of the droplets and the location where the water droplets are introduced can be chosen in relation to the rate of air flow over the heat exchanger and water evaporation rate.
- the droplet size may be managed, in part, by the augmentation unit pressure. Augmentation unit pressure can be monitored and controlled by controller 30.
- the refrigeration augmentation unit 300 may incorporate a deionizer and/or filter system (not shown) between water tank 310 and water droplet generator 360 in order to remove any undesirable ions and/or particulate matter from the water prior to forming and delivering the water droplets.
- Deionization may reduce or eliminate the deposition of undesirable materials on the heat rejection exchanger 34. Filtration can also prevent the deposition of undesirable materials on the heat rejection exchanger 34. Undesirable materials, such as metal salt deposits, may cause corrosion and reduce the ability of the heat rejection exchanger to facilitate heat transfer from the refrigerant to the passing air. Furthermore, undesirable materials can clog the water droplet generator 360, resulting in a system with reduced efficacy.
- the water tank 310 may include an antimicrobial material.
- exemplary materials include a foam that provides a source of silver and/or copper ions to the water.
- the foam may be part of a cartridge or other device that allows for replenishment.
- the tank may be lined with a material that provides a source of silver or copper ions.
- Silver and copper ions can have an inhibitory effect on bacterial growth. It is also contemplated that water may be exposed to silver ions, copper ions, or both after leaving the water tank 310 but prior to being formed into droplets.
- Water may be provided to the water tank 310 by one or more of the following sources: collected from the evaporator in collector 48, from the exhaust gas outlet of the fuel cell 400 (when present), filled from a source external to the transportation refrigeration system 200. While one water tank 310 is shown for simplicity, it should be noted that multiple collection/storage containers may be used. Sources external to the transportation refrigeration system include tap water and water collected from the exhaust gas of a fuel cell used as part of propulsion motor 120. It will be appreciated that water supplied by the collector 48 may be dependent on the humidity of the refrigerated space and it may be necessary to supplement with an additional source.
- All or part of the refrigeration augmentation unit 300 may be modular and thus removable when desired due to climate conditions.
- the water tank 310 may be removed, for example when the transport refrigeration system is going to be exposed to temperatures below 0°C.
- the water droplet generator 360 may also be removed. It is also contemplated that any residual water in the water tank 310 and/or water droplet generator may be removed using compressed air.
- the compressed air may be provided by an external source or on-board source as described below.
- Water tank 310 may be pressurized by compressed air provided by fuel cell 400, when present, or other methods of pressurization.
- pressure to create the water droplets maybe provided by another source such as a pump, compressor, or both (not shown).
- pressure may be managed by the controller 30.
- the flow rate to the water droplet generator may be up to 1.5 liters per minute and may be chosen based on environmental factors. For example, under conditions of high relative humidity the flow rate would be decreased in order to achieve evaporation of the majority of the water droplets and limit condensation on the refrigerant heat rejection heat exchanger and/or sub cooler. These considerations may be part of an algorithm used by the controller 30 to maximize the effect of evaporative cooling and the overall efficiency of the system.
- the amount and/or presence of mist may be managed by the controller and used to provide an increase in cooling either prior to opening the doors to the refrigerated space, immediately following opening the doors to the refrigerated space, or both.
- the refrigeration augmentation unit may be operated to provide a cooling capacity boost after the doors to one or more compartments have been opened and closed. More specifically, the refrigeration augmentation unit may be used to boost the cooling capacity between access episodes when time between the access episodes is insufficient for the transport refrigeration system to reach a set point using the normal (non-augmented) cooling capacity of the system.
- the refrigeration augmentation unit is operational for a portion of these cycles.
- the transportation refrigeration unit completes a desired number of cycles, X.
- the refrigeration augmentation unit generates water droplets to cool the air entering the refrigerant heat rejection heat exchanger.
- X may be chosen based on the size of the fuel cell 400 (described below) so that fuel cell 400 generates enough water to provide the majority (or all) of the water for water droplet generation.
- the transport refrigeration unit 22 may be powered by a fuel cell 400 and/or an energy storage device 510.
- the fuel cell 400, associated fuel tanks 410, and energy storage device 510 may be attached to the trailer system 100.
- the fuel cell 400 may be located in transport refrigeration unit 22.
- the fuel cell 400, associated fuel tanks 410, and energy storage device 510 may be attached to a bottom of the trailer system 100.
- the fuel tanks 410 for the fuel cell 400 are understood by a person of skill in the art to be pressure vessels and the term "fuel tank" is not intended to refer to a diesel tank or a gasoline tank in this context.
- the fuel cell 400 includes an anode electrode and a cathode electrode separated by an electrolyte (not shown for simplicity).
- a reducing fluid such as hydrogen is supplied to the anode electrode, and an oxidant such as oxygen or air is supplied to the cathode electrode.
- the hydrogen electrochemically reacts at a catalyst surface of the anode electrode to produce hydrogen ions and electrons.
- the electrons are conducted to an external load circuit (e.g., the transport refrigeration unit 22 or energy storage device 510) and then returned to the cathode electrode, while the hydrogen ions transfer through the electrolyte to the cathode electrode, where they react with the oxidant and electrons to produce water and release thermal energy.
- a fuel tank 410 is configured to store and provide the reducing fluid to the fuel cell 400.
- the reducing fluid is hydrogen.
- the fuel cell 400 may be located inside the transport refrigeration unit 22, as shown in FIG. 2 . In another embodiment, the fuel cell 400 may be located outside of the transport refrigeration unit 22. The fuel cell 400 may be located under the transport container 106 of the trailer system 100.
- the fuel tank 410 may be located inside the transport refrigeration unit 22. In another embodiment, the fuel tank 410 may be located outside of the transport refrigeration unit 22. The fuel tank 410 may be located under the transport container 106 of the trailer system 100, as shown in FIG. 1 .
- one or more supplemental power sources 500 may be located outside of the transport refrigeration unit 22, as shown in FIG. 1 . In another embodiment, the one or more supplemental power sources 500 may be located within the transport refrigeration unit 22.
- the one or more supplemental power sources 500 may include an energy storage device, a thermal storage system, and/or an electric generation device.
- the fuel cell 400 may power the transport refrigeration unit 22 directly or may provide electricity to an energy storage device, which then provides power to the transport refrigeration unit 22.
- the thermal storage system does not directly provide electricity to the transport refrigeration unit 22 but rather the thermal storage system may be used to save electricity used by the transport refrigeration unit 22 by providing supplemental or replacement heating or cooling to the transport container 106, and/or to a sub-cooler of the refrigerant in the refrigeration system.
- a thermal storage system may be present to sink electrical energy into to cool the transport container 106.
- the thermal storage system may utilize a phase change material to provide cooling to the transport container 106.
- the thermal storage system may utilize electricity to change the phase change material from one phase to another phase to cool the transport container 106.
- the thermal storage system may be an ice generation system to create ice to cool the transport container 106.
- the ice generation system may generate ice when electricity is available or plentiful to provide lasting cooling for the transport container 106 to conserve electricity later by reducing use of the compression device 32 for cooling.
- the energy storage device may include a battery system, a capacitor, and/or any other electricity storage system known to one of skill in the art.
- the battery system may comprise chemical batteries, lithium-ion batteries, solid state batteries, flow batteries, or any other type of battery known to one of skill in the art.
- the battery system may employ multiple batteries organized into battery banks.
- the capacitor may be an electrolytic capacitor, a mica capacitor, a paper capacitor a film capacitor, a nonpolarized capacitor, a ceramic capacitor, or any type of capacitor known to one of skill in the art.
- the electricity generated by the electric generation device may charge the energy storage device or directly power the transport refrigeration unit 22.
- the electric generation device may include an axle generator, hub generator, and/or any other electricity generation system known to one of skill in the art.
- the energy storage device may be charged by a stationary charging station such as, for example a three-phase 460Vac (60Hz) or 400Vac (50Hz) power outlet.
- the charging station may provide single phase (e.g., level 2 charging capability) or three phase AC power to the energy storage device 510. It is understood that the charging station may have any phase charging and embodiments disclosed herein are not limited to single phase or three phase AC power.
- the transport refrigeration unit 22 has a plurality of electrical power demand loads on the energy storage device 510, including, but not limited to, the electric motor 26 for the compression device 32, the drive motor 42 for the fan 40 associated with the refrigerant heat rejection heat exchanger 34, and the drive motor 46 for the fan 44 associated with the refrigerant heat absorption heat exchanger 38.
- the fan motors 42, 46 and the electric motor 26 may be an AC motor or a DC motor, it is to be understood that various power converters 52, such as AC to DC rectifiers, DC to AC inverters, AC to AC voltage/frequency converters, DC to DC voltage converters, and filters, may be employed in connection with the energy storage device 150 as appropriate.
- the heater 48 also constitutes an electrical power demand load.
- the electric resistance heater 48 may be selectively operated by the controller 30 whenever a control temperature within the temperature controlled cargo box drops below a preset lower temperature limit, which may occur in a cold ambient environment. In such an event the controller 30 would activate the heater 48 to heat air circulated over the heater 48 by the fan(s) 44 associated with the refrigerant heat absorption heat exchanger 38. The heater 48 may also be used to deice the refrigerant heat absorption heat exchanger 38. Additionally, the electric motor 26 being used to power the refrigerant compression device 32 constitutes a demand load.
- the refrigerant compression device 32 may comprise a single-stage or multiplestage compressor such as, for example, a reciprocating compressor or a scroll compressor.
- the transport refrigeration system 200 may also include a voltage sensor 28 to sense the voltage and phase coming into the transport refrigeration unit 22. Additional power demand loads may include various controllers, battery chargers, stepper motor modules, display modules, power control modules, control box, refrigerant valves, coolant pumps, and any component of the transport refrigeration system 200 that may require power or accessories of 106, such as lift gate.
- the power demand loads of the transport refrigeration unit 22 may be managed and fulfilled by an energy management system (not shown).
- the energy management system may include the fuel cell 400 and/or the one or more supplemental power sources 500.
- the energy management system may include a power management module that is in communication with transport refrigeration unit 22, the fuel cell 400 and/or the one or more supplemental power sources 500, and the fuel tank.
- FIGS. 3A-C and FIGS. 4A-C show the effect of different amounts of evaporative cooling (indicated by the relative humidity after spray evaporative cooling) on the coefficient of performance (COP), cooling capacity, and power.
- FIGS. 3A-C show the effect at an ambient temperature of 40°C, a return air temperature of 0°C in the conditioned space and a variety of ambient relative humidity values.
- FIGS. 4A-C show the effect of evaporative cooling at an ambient temperature of 40°C, a return air temperature of -30°C in the conditioned space and a variety of ambient relative humidity values.
- FIGS. 3A-C and FIGS. 4A-C both show that evaporative cooling increases the COP and cooling capacity while simultaneously reducing the required power at all ambient relative humidity values less than 1 (less than 100% relative humidity). Additionally, the greater the relative humidity after evaporative cooling the greater the effect.
- the transportation refrigeration system having a refrigeration augmentation unit 300 can generate more cooling capacity at less power when using the refrigeration augmentation unit. Accordingly, described herein is a method of cooling a refrigerated cargo space. The method includes cycling a transportation refrigeration system having a fuel cell and a refrigeration augmentation unit on and off for a specified number of times without using the refrigeration augmentation unit; collecting water from the fuel cell during the transportation refrigeration system cycling; and operating the transportation refrigeration system and the refrigeration augmentation unit using the collected water.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- Health & Medical Sciences (AREA)
- Public Health (AREA)
- Transportation (AREA)
- Manufacturing & Machinery (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Devices That Are Associated With Refrigeration Equipment (AREA)
Abstract
Description
- The embodiments herein generally relate to transport refrigeration.
- Refrigerated vehicles, containers and trailers are commonly used to transport perishable goods. A transport refrigeration unit is commonly mounted to the vehicle, container, or to the trailer in operative association with a cargo space defined within the vehicle, container or trailer for maintaining one or more controlled temperature environments within the cargo space.
- Conventionally, transport refrigeration units used in connection with refrigerated vehicles and refrigerated trailers include a refrigerant compressor, a condenser with one or more associated condenser fans, an expansion device, and one or more evaporators with one or more associated evaporator fans, which are connected via appropriate refrigerant lines in a closed refrigerant flow circuit. Air or an air/ gas mixture is drawn from the interior volume of the cargo space by means of the evaporator fan(s) associated with the evaporator, passed through the airside of the evaporator in heat exchange relationship with refrigerant whereby the refrigerant absorbs heat from the air, thereby cooling the air. The cooled air is then supplied back to the cargo space. In cases where there are multiple compartments, each compartment may have an evaporator and an associated evaporator fan.
- Heat from a truck connected to the refrigerated trailer or container can make the area between the truck and refrigerated trailer or container approximately 10°C or more higher than the ambient environment. Given the fact that the condenser is typically located in this area, the increased temperature of this area (typically referred to as a heat island) makes the transfer of heat from the refrigerant in the condenser to the surrounding air more difficult. Improved methods of transferring heat from the refrigerant in the condenser are desired.
- Viewed from a first aspect, the present invention provides a transportation refrigeration system including:a transportation refrigeration unit configured to maintain a temperature in a refrigerated cargo space and comprising a refrigerant expansion device, a refrigerant heat absorption heat exchanger, a refrigerant compression device, and a refrigerant heat rejection heat exchanger; and a refrigeration augmentation unit comprising a water tank having an outlet, and a water droplet generator in fluid communication with a water tank outlet and configured to disperse water droplets into an air stream flowing to the refrigerant heat rejection heat exchanger.
- In addition to one or more of the features described above, further embodiments may include a fuel cell having an exhaust gas outlet in fluid communication with the water tank.
- In addition to one or more of the features described above, further embodiments may include a refrigeration augmentation unit which is removable.
- In addition to one or more of the features described above, further embodiments may include a deionizer disposed between the water tank and the water droplet generator.
- In addition to one or more of the features described above, further embodiments may include the refrigeration augmentation unit including an antimicrobial material.
- In addition to one or more of the features described above, further embodiments may include the water tank having an inlet connected to an exhaust gas outlet of a fuel cell that is part of a propulsion motor.
- In addition to one or more of the features described above, further embodiments may include the transportation refrigeration unit located in a heat island.
- Viewed from a second aspect, the present invention provides a transportation refrigeration system including a transportation refrigeration unit configured to maintain a temperature in a refrigerated cargo space and comprising a refrigerant expansion device, refrigerant heat absorption heat exchanger, a refrigerant compression device, and a refrigerant heat rejection heat exchanger; a refrigeration augmentation unit comprising a water tank having an inlet, an outlet, a water droplet generator in fluid communication with the water tank outlet and configured to disperse water droplets into an air stream flowing to the refrigerant heat rejection heat exchanger; and a controller which controls the operation of the refrigeration augmentation unit based on ambient conditions and transportation refrigeration system conditions to disperse water droplets in a quantity and size that will result in evaporation of greater than or equal to 75% of the water droplets evaporate before contact with the refrigerant heat rejection heat exchanger.
- In addition to one or more of the features described above, further embodiments may include a fuel cell having an exhaust gas outlet in fluid communication with the inlet of the water tank.
- In addition to one or more of the features described above, further embodiments may include a deionizer disposed between the water tank and the spray nozzle.
- In addition to one or more of the features described above, further embodiments may include the refrigeration augmentation unit further including an antimicrobial material.
- In addition to one or more of the features described above, further embodiments may include the water tank having an inlet connected to an exhaust gas of a fuel cell located as part of a propulsion motor.
- In addition to one or more of the features described above, further embodiments may include the controller configured control operation such that greater than or equal to 90% of the water droplets evaporate before contact with the refrigerant heat rejection heat exchanger.
- In addition to one or more of the features described above, the water droplet generator includes an ultrasonic droplet generator.
- Viewed from a third aspect, the present invention provides a method of cooling a refrigerated cargo space including: cycling a transportation refrigeration system on and off for a specified number of times wherein the transportation refrigeration system has a fuel cell, a controller, and a refrigeration augmentation unit and cycling is without using the refrigeration augmentation unit; and collecting water from the fuel cell during the transportation refrigeration system cycling without using the refrigeration augmentation unit; and cycling the transportation refrigeration system using the refrigeration augmentation unit, wherein water used by the refrigeration augmentation unit is the collected water.
- In addition to one or more of the features described above, water may also be collected from a propulsion motor fuel cell.
- In addition to one or more of the features described above, water may also be collected from a refrigerant heat absorption heat exchanger.
- In addition to one or more of the features described above, the controller may control the operation of the refrigeration augmentation unit based on ambient conditions and transportation refrigeration system conditions to disperse water droplets in a quantity and size that will result in evaporation of greater than or equal to 75% of the water droplets evaporate before contact with the refrigerant heat rejection heat exchanger.
- In addition to one or more of the features described above, the transportation refrigeration system may be located in a heat island.
- The foregoing features and elements may be combined in various combinations without exclusivity, unless expressly indicated otherwise. These features and elements as well as the operation thereof will become more apparent in light of the following description and the accompanying drawings. It should be understood, however, that the following description and drawings are intended to be illustrative and explanatory in nature and non-limiting.
- The following descriptions should not be considered limiting in any way. With reference to the accompanying drawings, like elements are numbered alike:
-
FIG. 1 shows a schematic illustration of a transport refrigeration system; -
FIG. 2 shows an enlarged schematic illustration of the transport refrigeration system ofFIG. 1 ; -
FIG. 3A-C are graphs of the effect of evaporative cooling on coefficient of performance, cooling capacity and power at an ambient temperature of 40°C, a return air temperature of 0°C, and a variety of ambient relative humidity values; and -
FIG. 4A-C are graphs of the effect of evaporative cooling on coefficient of performance, cooling capacity and power at ambient temperature of 40°C, a return air temperature of -30°C, and a variety of ambient relative humidity values. - A detailed description of one or more embodiments of the disclosed apparatus and method are presented herein by way of exemplification and not limitation with reference to the Figures.
- On many commercially available transport refrigeration units the compressor, and typically other components of the transport refrigeration unit, is powered during transit by a prime mover, either through a direct mechanical coupling or a belt drive. Alternatively, the transport refrigeration unit may be electrically powered (e.g., using an alternating current (AC) synchronous generator that generates AC power). The generated AC power is typically used to power an electric motor for driving the refrigerant compressor, and other components of the transport refrigeration unit. In a different electrically powered transport refrigeration unit, the AC generator may be replaced with a battery pack to provide power to the loads. Alternatively, a fuel cell may provide power to the loads. In each of these cases, the condenser of the transport refrigeration unit is typically located on the outside wall of the trailer in the area between the trailer and the truck. This area has temperatures that may be greater than or equal to 10°C higher than the ambient outdoor temperature, creating a heat island and making heat transfer from the refrigerant to the ambient outdoor less energetically favorable, decreasing the efficiency of the refrigeration unit as a whole.
- Improved heat transfer at the condenser can be achieved by incorporating evaporative cooling at the refrigerant heat rejection heat exchanger (condenser). Water droplets are sprayed onto the refrigerant heat rejection heat exchanger or into the air directly adjacent to the refrigerant heat rejection heat exchanger. Most or all of the water evaporates, and the phase change decreases the air temperature. The lower temperature air can accept more heat than the higher temperature air which increases the amount of heat that can be removed from the refrigerant in the refrigerant heat rejection heat exchanger. Stated another way, the resulting increase in the temperature difference between the condenser and the air flowing across the condenser results in an increase in the heat transfer rate. With increased heat transfer rate, the energy efficiency of the system overall is improved. In cases where a prime mover, generator or battery provides power to the transportation refrigeration unit, water may be provided from an externally filled tank, collected from the refrigerant heat absorption heat exchanger(s) (evaporator(s)) or both. In cases where a fuel cell system provides power to the transportation refrigeration unit, water may be provided by the exhaust gas of the fuel cell system optionally in combination with water collected from the refrigerant heat absorption heat exchanger, for example when water is collected during a defrost operation(s). It is further contemplated that in some embodiments, a truck and trailer combination may include a truck using a fuel cell system as a power source and water from the exhaust gas of the truck fuel cell system may provide water to the refrigerant heat rejection heat exchanger water spray.
- Referring to
FIGS. 1 and2 , various embodiments are illustrated.FIG. 1 shows a schematic illustration of atransport refrigeration system 200.FIG. 2 shows an enlarged schematic illustration of thetransport refrigeration system 200 ofFIG. 1 . - The
transport refrigeration system 200 is being illustrated as atrailer system 100, as seen inFIG. 1 . Thetrailer system 100 includes avehicle 102 coupled to atransport container 106. Thevehicle 102 may include an operator's compartment orcab 104 and apropulsion motor 120 which acts as the drive system of thetrailer system 100. Thepropulsion motor 120 is configured to power thevehicle 102. The energy source that powers thepropulsion motor 120 may be at least one of compressed natural gas, liquefied natural gas, gasoline, electricity, diesel, hydrogen, electricity from a fuel cell, electricity from a hydrogen fueled proton exchange membrane (PEM) fuel cell, electricity from a battery, electricity from a generator, or any combination thereof. Thepropulsion motor 120 may be an electric motor or a hybrid motor (e.g., a combustion engine and an electric motor). Thetransport container 106 may be removably coupled to thevehicle 102. Thetransport container 106 is a refrigerated trailer and includes a top wall 108, a directly opposedbottom wall 110, opposedside walls 112, and afront wall 114, with thefront wall 114 being closest to thevehicle 102. Thetransportation refrigeration unit 22 is located on thefront wall 114, between thetransport container 106 and thevehicle 102. This placement results in the transportation refrigeration unit being located in a heat island. Heat island, as used herein, describes an area or space in which has a temperature at least 5-10°C higher than the ambient temperature. Thetransport container 106 further includes a door ordoors 117 at arear wall 116, opposite thefront wall 114. Alternatively, door ordoors 117 may be located on one ormore side walls 112. It is further contemplated that door ordoors 117 may be located on a combination of side wall(s) 112 andrear wall 116. The walls of thetransport container 106 define arefrigerated cargo space 119. Therefrigerated cargo space 119 may comprise multiple compartments which may have different desired conditions such as different temperatures. For simplicity, a singlerefrigerated cargo space 119 is referred to herein. It is appreciated by those of skill in the art that embodiments described herein may be applied to a tractor-trailer refrigerated system or non-trailer refrigeration such as, for example a rigid truck, a truck having refrigerated compartment, or a shipping container having a refrigerated compartment. - Typically,
transport refrigeration systems 200 are used to transport and distribute perishable goods and environmentally sensitive goods (herein referred to as perishable goods 118). Theperishable goods 118 may include but are not limited to fruits, vegetables, grains, beans, nuts, eggs, dairy, seed, flowers, meat, poultry, fish, ice, blood, pharmaceuticals, or any other suitable cargo requiring temperature controlled transport. Thetransport refrigeration system 200 includes atransport refrigeration unit 22, arefrigerant compression device 32, anelectric motor 26 for driving therefrigerant compression device 32, and a controller 30. While shown as a single controller, controller 30 may comprise one or more sub controllers (not shown) which are coordinated to control elements of thetransport refrigeration system 200. Thetransport refrigeration unit 22 is in operative association with therefrigerated cargo space 119 and is configured to provide conditioned air to thetransport container 106. Thetransport refrigeration unit 22 functions, under the control of the controller 30, to establish and regulate a desired environmental parameters, such as, for example temperature, pressure, humidity, carbon dioxide, ethylene, ozone, light exposure, vibration exposure, and other conditions in the refrigeratedcargo space 119, as known to one of ordinary skill in the art. In an embodiment, thetransport refrigeration unit 22 is capable of providing a desired temperature, carbon dioxide, and humidity range. - The
transport refrigeration unit 22 includes arefrigerant compression device 32, a refrigerant heat rejection heat exchanger (also referred to as a condenser) 34, anexpansion device 36, and a refrigerant heat absorption heat exchanger (also referred to as an evaporator) 38 connected in refrigerant flow communication in a closed loop refrigerant circuit and arranged in a conventional refrigeration cycle. Thetransport refrigeration unit 22 also includes one ormore fans 40 associated with the refrigerant heatrejection heat exchanger 34 and driven by fan motor(s) 42 and one ormore fans 44 associated with the refrigerant heatabsorption heat exchanger 38 and driven by fan motor(s) 46. Thetransport refrigeration unit 22 may also include a heater (not shown) associated with the refrigerant heatabsorption heat exchanger 38. The heater may be an electric resistance heater. It is to be understood that other components (not shown) may be incorporated into the refrigerant circuit as desired, including for example, but not limited to, a suction modulation valve, a receiver, a filter/dryer, a sub cooler, and an economizer circuit. - The refrigerant heat
rejection heat exchanger 34 may, for example, comprise one or more refrigerant conveying coiled tubes or one or more tube banks formed of a plurality of refrigerant conveying tubes across flow path to theheat outlet 142. The fan(s) 40 are operative to pass air, typically ambient air, across the tubes of the refrigerant heatrejection heat exchanger 34 to cool refrigerant vapor passing through the tubes. The refrigerant heatrejection heat exchanger 34 may operate either as a refrigerant condenser, such as if thetransport refrigeration unit 22 is operating in a subcritical refrigerant cycle or as a refrigerant gas cooler, such as if thetransport refrigeration unit 22 is operating in a transcritical cycle. A sub cooler, when present, receives refrigerant from the refrigerant heat rejection heat exchanger. - The refrigerant heat
absorption heat exchanger 38 may, for example, also comprise one or more refrigerant conveying coiled tubes or one or more tube banks formed of a plurality of refrigerant conveying tubes extending across flow path from areturn air intake 136. The fan(s) 44 are operative to pass air drawn from the refrigeratedcargo space 119 across the tubes of the refrigerant heatabsorption heat exchanger 38 to heat and evaporate refrigerant liquid passing through the tubes and cool the air. The air cooled in traversing the refrigerant heatabsorption heat exchanger 38 is supplied back to the refrigeratedcargo space 119 through arefrigeration unit outlet 140. It is to be understood that the term "air" when used herein with reference to the atmosphere within the cargo box includes mixtures of air with other gases, such as for example, but not limited to, nitrogen or carbon dioxide, sometimes introduced into a refrigerated cargo box for transport of perishable produce. - Airflow is circulated into and through the refrigerated
cargo space 119 of thetransport container 106 by means of thetransport refrigeration unit 22. Areturn airflow 134 flows into thetransport refrigeration unit 22 from the refrigeratedcargo space 119 through the refrigeration unitreturn air intake 136, and across the refrigerant heatabsorption heat exchanger 38 via thefan 44, thus conditioning thereturn airflow 134 to a selected or predetermined temperature. The conditionedreturn airflow 134, now referred to assupply airflow 138, is supplied into therefrigerated cargo space 119 of thetransport container 106 through therefrigeration unit outlet 140. -
Heat 135 is removed from the refrigerant heatrejection heat exchanger 34 through theheat outlet 142. Thetransport refrigeration unit 22 may contain anexternal air inlet 144, as shown inFIG. 2 , to aid in the removal ofheat 135 from the refrigerant heatrejection heat exchanger 34 by pulling inexternal air 137. Thesupply airflow 138 may cool theperishable goods 118 in the refrigeratedcargo space 119 of thetransport container 106. - It is to be appreciated that the
transport refrigeration unit 22 can further be operated in reverse to warm thetransport container 106 when, for example, the outside temperature is very low. In the illustrated embodiment, thereturn air intake 136, therefrigeration unit outlet 140, theheat outlet 142, and theexternal air inlet 144 are configured as grilles to help prevent foreign objects from entering thetransport refrigeration unit 22. - The
transport refrigeration system 200 also includes a controller 30 configured for controlling the operation of thetransport refrigeration system 200 including, but not limited to, the operation of various components of therefrigerant unit 22 to provide and maintain a desired thermal environment within the refrigeratedcargo space 119. The controller 30 may also be able to selectively operate theelectric motor 26. The controller 30 may also be configured to provide a feedforward signal to thefuel cell 400 so that it will start up before thetransport refrigeration unit 22 places a load on thefuel cell 400. As mentioned above, controller 30 may comprises one or more sub controllers. - The controller 30 may be an electronic controller including a processor and an associated memory comprising computer-executable instructions that, when executed by the processor, cause the processor to perform various operations. The processor may be but is not limited to a single-processor or multi-processor system of any of a wide array of possible architectures, including field programmable gate array (FPGA), central processing unit (CPU), application specific integrated circuits (ASIC), digital signal processor (DSP) or graphics processing unit (GPU) hardware arranged homogenously or heterogeneously. The memory may be a storage device such as, for example, a random access memory (RAM), read only memory (ROM), or other electronic, optical, magnetic or any other computer readable medium. The controller 30 may have multiple inputs (e.g. analog, digital, others) and multiple outputs and a communication interface (e.g. CAN-bus, ethernet). The controller may also have circuits to protect the controller from inductive loads. The communication interface may include an interface that allows data about the operation of the transport refrigeration system to be transmitted to a remote server (e.g., the cloud) for storage and/or analysis and which also can be used to receive instructions from a remote location e.g., a remote operator or a remote server. Exemplary instructions include initiating operation of the refrigeration augmentation unit and halting operation of the refrigeration augmentation unit.
- The
transport refrigeration system 200 also includes arefrigeration augmentation unit 300. Refrigeration augmentation unit includes awater tank 310 and a water droplet generator(s) 360 for dispersing water droplets into the air stream flowing to the refrigerantheat rejection exchanger 34, directly on the surface of the refrigerantheat rejection exchanger 34, or a combination thereof. In cases where the refrigerant heat rejection exchanger includes a sub cooler (not shown) the water droplets may be dispersed in the airstream flowing to the sub cooler, directly on the surface of the sub cooler, or a combination thereof. Exemplary water droplet generators include spray nozzles and ultrasonic droplet generators such as ultrasonication mist generators. Exemplary maximum droplet size is less than or equal to 100 micrometers (µm), or less than or equal to 50 µm. - The water droplet generator(s) may disperse the water droplets in any combination of orientations. In some embodiments, a combination of orientations is desired to facilitate mixing with the air flow and facilitate evaporation. Water droplet evaporation reduces the temperature of the air passing over the refrigerant heat rejection exchanger. By reducing the temperature of the air passing over the refrigerant
heat rejection exchanger 34 the heat transfer rate from the refrigerant passing through the refrigerantheat rejection exchanger 34 can be increased. The water droplets are sized so that at least 75%, or at least 85%, or at least 90 volume% (vol%) of the droplets evaporate. As can be appreciated, the size of the droplets and the location where the water droplets are introduced (such as the distance from the refrigerant heat rejection heat exchanger or sub cooler) can be chosen in relation to the rate of air flow over the heat exchanger and water evaporation rate. The droplet size may be managed, in part, by the augmentation unit pressure. Augmentation unit pressure can be monitored and controlled by controller 30. - The
refrigeration augmentation unit 300 may incorporate a deionizer and/or filter system (not shown) betweenwater tank 310 andwater droplet generator 360 in order to remove any undesirable ions and/or particulate matter from the water prior to forming and delivering the water droplets. Deionization may reduce or eliminate the deposition of undesirable materials on theheat rejection exchanger 34. Filtration can also prevent the deposition of undesirable materials on theheat rejection exchanger 34. Undesirable materials, such as metal salt deposits, may cause corrosion and reduce the ability of the heat rejection exchanger to facilitate heat transfer from the refrigerant to the passing air. Furthermore, undesirable materials can clog thewater droplet generator 360, resulting in a system with reduced efficacy. - Additionally, the
water tank 310 may include an antimicrobial material. Exemplary materials include a foam that provides a source of silver and/or copper ions to the water. The foam may be part of a cartridge or other device that allows for replenishment. Alternatively, the tank may be lined with a material that provides a source of silver or copper ions. Silver and copper ions can have an inhibitory effect on bacterial growth. It is also contemplated that water may be exposed to silver ions, copper ions, or both after leaving thewater tank 310 but prior to being formed into droplets. - Water may be provided to the
water tank 310 by one or more of the following sources: collected from the evaporator incollector 48, from the exhaust gas outlet of the fuel cell 400 (when present), filled from a source external to thetransportation refrigeration system 200. While onewater tank 310 is shown for simplicity, it should be noted that multiple collection/storage containers may be used. Sources external to the transportation refrigeration system include tap water and water collected from the exhaust gas of a fuel cell used as part ofpropulsion motor 120. It will be appreciated that water supplied by thecollector 48 may be dependent on the humidity of the refrigerated space and it may be necessary to supplement with an additional source. - All or part of the
refrigeration augmentation unit 300 may be modular and thus removable when desired due to climate conditions. For example, thewater tank 310 may be removed, for example when the transport refrigeration system is going to be exposed to temperatures below 0°C. Thewater droplet generator 360 may also be removed. It is also contemplated that any residual water in thewater tank 310 and/or water droplet generator may be removed using compressed air. The compressed air may be provided by an external source or on-board source as described below. -
Water tank 310 may be pressurized by compressed air provided byfuel cell 400, when present, or other methods of pressurization. Alternatively, pressure to create the water droplets maybe provided by another source such as a pump, compressor, or both (not shown). As mentioned above, pressure may be managed by the controller 30. The flow rate to the water droplet generator may be up to 1.5 liters per minute and may be chosen based on environmental factors. For example, under conditions of high relative humidity the flow rate would be decreased in order to achieve evaporation of the majority of the water droplets and limit condensation on the refrigerant heat rejection heat exchanger and/or sub cooler. These considerations may be part of an algorithm used by the controller 30 to maximize the effect of evaporative cooling and the overall efficiency of the system. - The amount and/or presence of mist may be managed by the controller and used to provide an increase in cooling either prior to opening the doors to the refrigerated space, immediately following opening the doors to the refrigerated space, or both. In some embodiments the refrigeration augmentation unit may be operated to provide a cooling capacity boost after the doors to one or more compartments have been opened and closed. More specifically, the refrigeration augmentation unit may be used to boost the cooling capacity between access episodes when time between the access episodes is insufficient for the transport refrigeration system to reach a set point using the normal (non-augmented) cooling capacity of the system.
- It is also contemplated that in situations in which the
transport refrigeration unit 22 cycles between an "on" state and an "off' state, the refrigeration augmentation unit is operational for a portion of these cycles. For example, the transportation refrigeration unit completes a desired number of cycles, X. After X cycles the refrigeration augmentation unit generates water droplets to cool the air entering the refrigerant heat rejection heat exchanger. X may be chosen based on the size of the fuel cell 400 (described below) so thatfuel cell 400 generates enough water to provide the majority (or all) of the water for water droplet generation. - The
transport refrigeration unit 22 may be powered by afuel cell 400 and/or an energy storage device 510. Thefuel cell 400, associatedfuel tanks 410, and energy storage device 510 may be attached to thetrailer system 100. Thefuel cell 400 may be located intransport refrigeration unit 22. Alternatively, thefuel cell 400, associatedfuel tanks 410, and energy storage device 510 may be attached to a bottom of thetrailer system 100. Thefuel tanks 410 for thefuel cell 400 are understood by a person of skill in the art to be pressure vessels and the term "fuel tank" is not intended to refer to a diesel tank or a gasoline tank in this context. - The
fuel cell 400 includes an anode electrode and a cathode electrode separated by an electrolyte (not shown for simplicity). A reducing fluid such as hydrogen is supplied to the anode electrode, and an oxidant such as oxygen or air is supplied to the cathode electrode. In a cell utilizing a PEM as the electrolyte, the hydrogen electrochemically reacts at a catalyst surface of the anode electrode to produce hydrogen ions and electrons. The electrons are conducted to an external load circuit (e.g., thetransport refrigeration unit 22 or energy storage device 510) and then returned to the cathode electrode, while the hydrogen ions transfer through the electrolyte to the cathode electrode, where they react with the oxidant and electrons to produce water and release thermal energy. Afuel tank 410 is configured to store and provide the reducing fluid to thefuel cell 400. In an embodiment, the reducing fluid is hydrogen. - There may be one or
more fuel cells 400 and one ormore fuel tanks 410. In one embodiment, thefuel cell 400 may be located inside thetransport refrigeration unit 22, as shown inFIG. 2 . In another embodiment, thefuel cell 400 may be located outside of thetransport refrigeration unit 22. Thefuel cell 400 may be located under thetransport container 106 of thetrailer system 100. - In one embodiment, the
fuel tank 410 may be located inside thetransport refrigeration unit 22. In another embodiment, thefuel tank 410 may be located outside of thetransport refrigeration unit 22. Thefuel tank 410 may be located under thetransport container 106 of thetrailer system 100, as shown inFIG. 1 . - In one embodiment, one or more
supplemental power sources 500 may be located outside of thetransport refrigeration unit 22, as shown inFIG. 1 . In another embodiment, the one or moresupplemental power sources 500 may be located within thetransport refrigeration unit 22. The one or moresupplemental power sources 500 may include an energy storage device, a thermal storage system, and/or an electric generation device. Thefuel cell 400 may power thetransport refrigeration unit 22 directly or may provide electricity to an energy storage device, which then provides power to thetransport refrigeration unit 22. - The thermal storage system does not directly provide electricity to the
transport refrigeration unit 22 but rather the thermal storage system may be used to save electricity used by thetransport refrigeration unit 22 by providing supplemental or replacement heating or cooling to thetransport container 106, and/or to a sub-cooler of the refrigerant in the refrigeration system. A thermal storage system may be present to sink electrical energy into to cool thetransport container 106. The thermal storage system may utilize a phase change material to provide cooling to thetransport container 106. For example, the thermal storage system may utilize electricity to change the phase change material from one phase to another phase to cool thetransport container 106. The thermal storage system may be an ice generation system to create ice to cool thetransport container 106. The ice generation system may generate ice when electricity is available or plentiful to provide lasting cooling for thetransport container 106 to conserve electricity later by reducing use of thecompression device 32 for cooling. - The energy storage device may include a battery system, a capacitor, and/or any other electricity storage system known to one of skill in the art. The battery system may comprise chemical batteries, lithium-ion batteries, solid state batteries, flow batteries, or any other type of battery known to one of skill in the art. The battery system may employ multiple batteries organized into battery banks. The capacitor may be an electrolytic capacitor, a mica capacitor, a paper capacitor a film capacitor, a nonpolarized capacitor, a ceramic capacitor, or any type of capacitor known to one of skill in the art.
- The electricity generated by the electric generation device may charge the energy storage device or directly power the
transport refrigeration unit 22. The electric generation device may include an axle generator, hub generator, and/or any other electricity generation system known to one of skill in the art. - The energy storage device may be charged by a stationary charging station such as, for example a three-phase 460Vac (60Hz) or 400Vac (50Hz) power outlet. The charging station may provide single phase (e.g., level 2 charging capability) or three phase AC power to the energy storage device 510. It is understood that the charging station may have any phase charging and embodiments disclosed herein are not limited to single phase or three phase AC power.
- The
transport refrigeration unit 22 has a plurality of electrical power demand loads on the energy storage device 510, including, but not limited to, theelectric motor 26 for thecompression device 32, thedrive motor 42 for thefan 40 associated with the refrigerant heatrejection heat exchanger 34, and thedrive motor 46 for thefan 44 associated with the refrigerant heatabsorption heat exchanger 38. As each of thefan motors electric motor 26 may be an AC motor or a DC motor, it is to be understood thatvarious power converters 52, such as AC to DC rectifiers, DC to AC inverters, AC to AC voltage/frequency converters, DC to DC voltage converters, and filters, may be employed in connection with the energy storage device 150 as appropriate. In the depicted embodiment, theheater 48 also constitutes an electrical power demand load. Theelectric resistance heater 48 may be selectively operated by the controller 30 whenever a control temperature within the temperature controlled cargo box drops below a preset lower temperature limit, which may occur in a cold ambient environment. In such an event the controller 30 would activate theheater 48 to heat air circulated over theheater 48 by the fan(s) 44 associated with the refrigerant heatabsorption heat exchanger 38. Theheater 48 may also be used to deice the refrigerant heatabsorption heat exchanger 38. Additionally, theelectric motor 26 being used to power therefrigerant compression device 32 constitutes a demand load. Therefrigerant compression device 32 may comprise a single-stage or multiplestage compressor such as, for example, a reciprocating compressor or a scroll compressor. Thetransport refrigeration system 200 may also include avoltage sensor 28 to sense the voltage and phase coming into thetransport refrigeration unit 22. Additional power demand loads may include various controllers, battery chargers, stepper motor modules, display modules, power control modules, control box, refrigerant valves, coolant pumps, and any component of thetransport refrigeration system 200 that may require power or accessories of 106, such as lift gate. - The power demand loads of the
transport refrigeration unit 22 may be managed and fulfilled by an energy management system (not shown). The energy management system may include thefuel cell 400 and/or the one or moresupplemental power sources 500. The energy management system may include a power management module that is in communication withtransport refrigeration unit 22, thefuel cell 400 and/or the one or moresupplemental power sources 500, and the fuel tank. -
FIGS. 3A-C andFIGS. 4A-C show the effect of different amounts of evaporative cooling (indicated by the relative humidity after spray evaporative cooling) on the coefficient of performance (COP), cooling capacity, and power.FIGS. 3A-C show the effect at an ambient temperature of 40°C, a return air temperature of 0°C in the conditioned space and a variety of ambient relative humidity values.FIGS. 4A-C show the effect of evaporative cooling at an ambient temperature of 40°C, a return air temperature of -30°C in the conditioned space and a variety of ambient relative humidity values.FIGS. 3A-C andFIGS. 4A-C both show that evaporative cooling increases the COP and cooling capacity while simultaneously reducing the required power at all ambient relative humidity values less than 1 (less than 100% relative humidity). Additionally, the greater the relative humidity after evaporative cooling the greater the effect. - The transportation refrigeration system having a
refrigeration augmentation unit 300 can generate more cooling capacity at less power when using the refrigeration augmentation unit. Accordingly, described herein is a method of cooling a refrigerated cargo space. The method includes cycling a transportation refrigeration system having a fuel cell and a refrigeration augmentation unit on and off for a specified number of times without using the refrigeration augmentation unit; collecting water from the fuel cell during the transportation refrigeration system cycling; and operating the transportation refrigeration system and the refrigeration augmentation unit using the collected water. - The term "about" is intended to include the degree of error associated with measurement of the particular quantity based upon the equipment available at the time of filing the application. For example, "about" can include a range of ± 8% or 5%, or 2% of a given value.
- The terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the present invention. As used herein, the singular forms "a", "an" and "the" are intended to include the plural forms as well, unless the context clearly indicates otherwise. It will be further understood that the terms "comprises" and/or "comprising," when used in this specification, specify the presence of stated features, integers, steps, operations, elements, and/or components, but do not preclude the presence or addition of one or more other features, integers, steps, operations, element components, and/or groups thereof.
- While the present invention has been described with reference to an exemplary embodiment or embodiments, it will be understood by those skilled in the art that various changes may be made and equivalents may be substituted for elements of the described embodiments without departing from the scope of the present invention. In addition, many modifications may be made to adapt a particular situation or material to the teachings herein without departing from the scope of the present invention. Therefore, it is intended that the present invention not be limited to the particular embodiment disclosed, but that the present invention will include all embodiments falling within the scope of the claims.
- The following clauses set out aspects of the invention which may or may not presently be claimed, but which may form the basis for future amendments or a divisional application.
- 1. A transportation refrigeration system comprising: a transportation refrigeration unit configured to maintain a temperature in a refrigerated cargo space and comprising a refrigerant expansion device, refrigerant heat absorption heat exchanger, a refrigerant compression device, and a refrigerant heat rejection heat exchanger; a refrigeration augmentation unit comprising a water tank having an inlet, an outlet, a water droplet generator in fluid communication with the water tank outlet and configured to disperse water droplets into an air stream flowing to the refrigerant heat rejection heat exchanger; and a controller which controls the operation of the refrigeration augmentation unit based on ambient conditions and transportation refrigeration system conditions to disperse water droplets in a quantity and size that will result in evaporation of greater than or equal to 75% of the water droplets evaporate before contact with the refrigerant heat rejection heat exchanger.
- 2. The transportation refrigeration system of
clause 1, further comprising a fuel cell having an exhaust gas outlet in fluid communication with the inlet of the water tank. - 3. The transportation refrigeration system of
clause 1 or 2, wherein the refrigeration augmentation unit further comprises a deionizer disposed between the water tank and the spray nozzle. - 4. The transportation refrigeration system of any one of
clauses 1 to 3, wherein the refrigeration augmentation unit further comprises an antimicrobial material. - 5. The transportation refrigeration system of any one of
clauses 1 to 4, wherein the water tank has an inlet connected to an exhaust gas of a fuel cell located as part of a propulsion motor. - 6. The transportation refrigeration system of any one of
clauses 1 to 5, wherein greater than or equal to 90% of the water droplets evaporate before contact with the refrigerant heat rejection heat exchanger. - 7. The transportation refrigeration system of any one of
clauses 1 to 6, wherein water droplet generator comprises an ultrasonic droplet generator. - 8. The transportation refrigeration system of any one of
clauses 1 to 7, wherein the refrigeration augmentation unit is removable.
Claims (15)
- A transportation refrigeration system (200), comprising:a transportation refrigeration unit (22) configured to maintain a temperature in a refrigerated cargo space (119) and comprising a refrigerant expansion device (36), a refrigerant heat absorption heat exchanger (38), a refrigerant compression device (32), and a refrigerant heat rejection heat exchanger (34); anda refrigeration augmentation unit (300) comprising a water tank (310) having an outlet, and a water droplet generator (360) in fluid communication with a water tank outlet and configured to disperse water droplets into an air stream flowing to the refrigerant heat rejection heat exchanger.
- The transportation refrigeration system of claim 1, further comprising a fuel cell (400) having an exhaust gas outlet in fluid communication with the water tank.
- The transportation refrigeration system of claim 1 or 2, wherein the refrigeration augmentation unit is removable.
- The transportation refrigeration system of any one of claims 1 to 3, wherein the refrigeration augmentation unit further comprises a deionizer disposed between the water tank and the water droplet generator.
- The transportation refrigeration system any one of claims 1 to 4, wherein the refrigeration augmentation unit further comprises an antimicrobial material.
- The transportation refrigeration system of any one of claims 1 to 5, wherein the water tank has an inlet connected to an exhaust gas outlet of a fuel cell that is part of a propulsion motor (120).
- The transportation refrigeration system of any one of claims 1 to 6, wherein the transportation refrigeration unit is located in a heat island.
- The transportation refrigeration system of any one of claims 1 to 7, further comprising:
a controller (30) which controls the operation of the refrigeration augmentation unit based on ambient conditions and transportation refrigeration system conditions to disperse water droplets in a quantity and size that will result in evaporation of greater than or equal to 75% of the water droplets evaporate before contact with the refrigerant heat rejection heat exchanger. - The transportation refrigeration system of claim 8, wherein greater than or equal to 90% of the water droplets evaporate before contact with the refrigerant heat rejection heat exchanger.
- The transportation refrigeration system of claim 8 or 9, wherein water droplet generator comprises an ultrasonic droplet generator.
- A method of cooling a refrigerated cargo space (119), comprising:cycling a transportation refrigeration system (200) having a fuel cell (400), a controller (30), and a refrigeration augmentation unit (300) on and off for a specified number of times without using the refrigeration augmentation unit;collecting water from the fuel cell during the transportation refrigeration system cycling without using the refrigeration augmentation unit; andcycling the transportation refrigeration system using the refrigeration augmentation unit, wherein water used by the refrigeration augmentation unit comprises the collected water.
- The method of cooling a refrigerated cargo space of claim 11, wherein water is also collected from a propulsion motor fuel cell.
- The method of cooling a refrigerated cargo space of claim 11 or 12, wherein water is also collected from a refrigerant heat absorption heat exchanger (38).
- The method of cooling a refrigerated cargo space of any one of claims 11 to 13, wherein a controller controls the operation of the refrigeration augmentation unit based on ambient conditions and transportation refrigeration system conditions to disperse water droplets in a quantity and size that will result in evaporation of greater than or equal to 75% of the water droplets evaporate before contact with the refrigerant heat rejection heat exchanger.
- The method of cooling a refrigerated cargo space of any one of claims 11 to 14, wherein the transportation refrigeration system is located in a heat island.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US202263367671P | 2022-07-05 | 2022-07-05 |
Publications (1)
Publication Number | Publication Date |
---|---|
EP4303047A1 true EP4303047A1 (en) | 2024-01-10 |
Family
ID=87074800
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP23183165.2A Pending EP4303047A1 (en) | 2022-07-05 | 2023-07-03 | Transport refrigeration unit with heat island mitigation |
Country Status (3)
Country | Link |
---|---|
US (1) | US20240010116A1 (en) |
EP (1) | EP4303047A1 (en) |
CN (1) | CN117341441A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111183050B (en) * | 2017-06-06 | 2023-09-19 | 开利公司 | Transport refrigeration system |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0740732A (en) * | 1993-07-28 | 1995-02-10 | Nippondenso Co Ltd | Air-conditioner |
US20100307176A1 (en) * | 2009-06-03 | 2010-12-09 | Gm Global Technology Operations, Inc. | Water Cooled Condenser in a Vehicle HVAC System |
CN201779816U (en) * | 2010-09-13 | 2011-03-30 | 厦门金龙汽车空调有限公司 | Automobile air-conditioner heat recycling device |
US20220133932A1 (en) * | 2020-10-30 | 2022-05-05 | Hyundai Motor Company | Sterilizer for Car by Using HOCL and Control Method Thereof |
-
2023
- 2023-07-03 EP EP23183165.2A patent/EP4303047A1/en active Pending
- 2023-07-03 US US18/346,300 patent/US20240010116A1/en active Pending
- 2023-07-04 CN CN202310809913.7A patent/CN117341441A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0740732A (en) * | 1993-07-28 | 1995-02-10 | Nippondenso Co Ltd | Air-conditioner |
US20100307176A1 (en) * | 2009-06-03 | 2010-12-09 | Gm Global Technology Operations, Inc. | Water Cooled Condenser in a Vehicle HVAC System |
CN201779816U (en) * | 2010-09-13 | 2011-03-30 | 厦门金龙汽车空调有限公司 | Automobile air-conditioner heat recycling device |
US20220133932A1 (en) * | 2020-10-30 | 2022-05-05 | Hyundai Motor Company | Sterilizer for Car by Using HOCL and Control Method Thereof |
Also Published As
Publication number | Publication date |
---|---|
CN117341441A (en) | 2024-01-05 |
US20240010116A1 (en) | 2024-01-11 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP3856549B1 (en) | Electrical architecture for powering transportation refrigeration unit | |
US11415367B2 (en) | Mechanical subcooler with battery supplement | |
EP4212369A1 (en) | Transportation refrigeration unit with external dc generator power source | |
EP3856551A1 (en) | Transportation refrigeration unit with energy storage system and external dc power source | |
US11362379B2 (en) | Transportation refrigeration unit with integrated battery enclosure cooling | |
US20200391574A1 (en) | Battery powered transportation refrigeration unit with variable inverter | |
EP4303047A1 (en) | Transport refrigeration unit with heat island mitigation | |
US11137173B2 (en) | Hot gas bypass for battery pack cold start | |
US20230278390A1 (en) | Transport refrigeration units for primary and auxiliary applications | |
US11976862B2 (en) | Electrical architecture for powering multiple transport refrigeration units | |
US20210249182A1 (en) | Cooled transformer for an energy storage device | |
US20230271480A1 (en) | Hybridized fuel cell transport refrigeration units | |
EP4303060A1 (en) | Voltage discharge in refrigeration system | |
US20230282857A1 (en) | Fuel cell health and safety system for transport refrigeration units | |
EP4309928A1 (en) | Fuel cell architecture for transport refrigeration unit | |
US20220072933A1 (en) | Multi charging system architecture | |
US20230271476A1 (en) | Transport refrigeration system having direct current power sources | |
EP4238794A1 (en) | Modular architecture for fuel cell powered transport refrigeration |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION HAS BEEN PUBLISHED |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC ME MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE |
|
17P | Request for examination filed |
Effective date: 20240709 |
|
RBV | Designated contracting states (corrected) |
Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC ME MK MT NL NO PL PT RO RS SE SI SK SM TR |